NO123726B - - Google Patents
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- Publication number
- NO123726B NO123726B NO401769A NO401769A NO123726B NO 123726 B NO123726 B NO 123726B NO 401769 A NO401769 A NO 401769A NO 401769 A NO401769 A NO 401769A NO 123726 B NO123726 B NO 123726B
- Authority
- NO
- Norway
- Prior art keywords
- roasting
- content
- magnetite
- post
- chlorinating
- Prior art date
Links
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 17
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 7
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 7
- 229910052742 iron Inorganic materials 0.000 claims description 7
- 238000007254 oxidation reaction Methods 0.000 claims description 7
- 229910052717 sulfur Inorganic materials 0.000 claims description 5
- 239000011593 sulfur Substances 0.000 claims description 5
- 230000029087 digestion Effects 0.000 claims description 4
- 230000014759 maintenance of location Effects 0.000 claims 1
- 239000002699 waste material Substances 0.000 description 6
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000002386 leaching Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 229910052595 hematite Inorganic materials 0.000 description 3
- 239000011019 hematite Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 3
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- -1 ferrous metals Chemical class 0.000 description 2
- 235000013980 iron oxide Nutrition 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 206010012335 Dependence Diseases 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
- C22B1/08—Chloridising roasting
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Compounds Of Iron (AREA)
Description
Fremgangsmåte for forbedring av oppslutningen Procedure for improving attendance
av klorerende røstet, ikke-jernmetallholdig of chlorinating roasted non-ferrous metals
kisavbrand med høyt magnetittinnhold. slag with a high magnetite content.
Foreliggende oppfinnelse vedrører en fremgangsmåte for forbedring av oppslutningen og for å forhøye gjennomgangsmengden ved den klorerende røstning av fra røstningen av sulfidiske jernmalmer stammende ikke-jern-metallholdig avbrand med høyt raagne-tittinnhold. The present invention relates to a method for improving digestion and for increasing the throughput during the chlorinating roasting of non-ferrous metal-containing waste with a high raagne-tite content originating from the roasting of sulphidic iron ores.
Svovelsyrefremstillingen fra sulfidiske jernmalmer er bare økonomisk når den ved røstningen erholdte avbrand videre an-vendes. Hertil er fjernelsen resp. utvinningen av de som regel sammensluttede ledsagende elementer nødvendig, for å kunne anven-de de jernoksyder som utgjør.hovedbestanddelen for masovnproses-sen. Den fremgangsmåte som beskjeftiger seg med utvinningen av de verdifulle stoffer og med finrensningen av jernmalmene, er så- .. ledes en viktig del ved den økonomiske fremstilling av svovel-Kfr. kl. 18a-l/02 syre fra sulfidiske jernmalmer. Prosessen betjener seg i overveiende grad av den klorerende røstning av avbranden med en et-terfølgende utlutning av røstegodset, hvorunder det som puffer-malm betegnede, rensede jernoksyd blir tilbake. The manufacture of sulfuric acid from sulphidic iron ores is only economical when the tailings obtained during roasting are further used. In addition, the removal or the recovery of the accompanying elements, which are generally joined together, is necessary, in order to be able to use the iron oxides which constitute the main component for the blast furnace process. The procedure which deals with the extraction of the valuable substances and with the fine purification of the iron ores is thus an important part of the economic production of sulphur-Kfr. at 18a-l/02 acid from sulphidic iron ores. The process is predominantly operated by the chlorinating roasting of the waste with a subsequent leaching of the roasting, during which the purified iron oxide designated as puffer ore remains.
Det er kjent at man blander avbranden for den klorerende røstning med koksalt og røster i etasjeovner, hvorunder i lø-pet av avrustningen av det gjenværende sulfidsvovel med sulfati-serings/ og kloreringsreaksjoner overføres de først tungtoppløse-lige ikke-jernmetallforbindelser, f.eks. sulfider resp. ferrit- It is known that the waste for the chlorinating roasting is mixed with common salt and roasted in floor furnaces, during which, in the course of the disarmament of the remaining sulphide sulfur with sulphation/ and chlorination reactions, the initially poorly soluble non-ferrous metal compounds are transferred, e.g. sulphides or ferrite
ter av kobber, sink og kobolt, til vann- resp. syreoppløselige forbindelser og herved gjøres tilgjengelig for en adskillelse og utvinning ved hjelp av utlutning. ter of copper, zinc and cobalt, for water or acid-soluble compounds and are thereby made available for separation and recovery by means of leaching.
Etter en fremgangsmåte som tilhører søkeren og som ikke hører til teknikkens nivå er oppnåelsen av optimale oppslutnings-resultater, dvs. lavest mulige restinnhold av kobber og sink i purpurmalmen, bundet til et ganske bestemt reaksjonsforløp, hvorunder den mulige gjennomgangsmengde i overveiende grad bestemmes av sulfidsvovelinnholdet i malegodsblandingen.. According to a method which belongs to the applicant and which does not belong to the state of the art, the achievement of optimal digestion results, i.e. the lowest possible residual content of copper and zinc in the purple ore, is tied to a fairly specific course of reaction, during which the possible throughput is predominantly determined by the sulphide sulfur content in the paint mixture..
Det finnes nu en rekke sorter av avbrand som ved sitt forhold ved den klorerende oppslutningsrøstning tydelig fremhever seg fra området for de kjente avhengigheter. Felles for alle- er et høyt magnetittinnhold som bevirker en nedsettelse av den mulige gjennomgangsmengde, og således ved inntil 30% ved rent magnetittavbrand, og uønsket høyere innhold av såkalte buntmetall-res-ter , særlig ved sink, og sulfatiseringsgraden, dvs. andelen av sulfidsvovelet som omdannes til sulfat, nedsettes. There are now a number of types of combustion which, by their relation to the chlorinating support vote, clearly stand out from the area of the known addictions. Common to all is a high magnetite content, which causes a reduction in the possible throughput, and thus by up to 30% in the case of pure magnetite combustion, and an undesired higher content of so-called bundle metal residues, especially in the case of zinc, and the degree of sulphation, i.e. the proportion of the sulphide sulphur, which is converted to sulphate, is reduced.
Magneittinnholdet i avbranden avhenger av arten for den for røstningen av de sulfidiske jernmalmer anvendte fremgangsmå-ter og de for gjennomføringen til enhver tid gitte betingelser. The magnetite content in the waste depends on the nature of the methods used for the roasting of the sulphidic iron ores and the conditions given for the execution at any given time.
Som regel har de fra etasjeovner resulterende avbrander lavere magnetittinnhold (omtrent 4-10%) enn de fra hvirvelskiktovner erholdte materialer' (12-18 %) . Ennu høyere verdier oppviser avbrand som fåes ved bestemte, for arsen- og blyfjernelse utviklede to- As a rule, the slag resulting from floor furnaces has a lower magnetite content (approximately 4-10%) than the materials obtained from fluidized bed furnaces (12-18%). Even higher values show burn-off that is obtained from specific, developed for arsenic and lead removal
og én-trinnede hvirvelprosesser, hvorunder det ved sistnevnte fåes praktisk talt ren magnetittavbrand. and one-stage vortex processes, during which practically pure magnetite combustion is obtained in the latter.
Fra det spanske patentskrift 338 663 er det kjent å under-kaste avbrand med høyt innhold av magnetitt før den klorerende resp. sulfatiserende røstning en etteroksydas jon, hvorved magnetitt i vidtgående grad skal omdannes til hematitt.Det spanske patentskrift inneholder ingen nærmere angivelser angående oksydasjonsgraden, dvs. man kan ikke ut fra patentskriftet utlede nærmere hvor langt magnetitten skal omdannes til hematitt. Omdanner man nemlig magnetitt fullstendig til hematitt, så inneholder den etteroksyderte avbrand praktisk talt ikke mere noe sulfidsvovel, slik at en klorerende og sulfatiserende røstning ikke mere er mulig. From the Spanish patent document 338 663, it is known to submit to combustion with a high content of magnetite before the chlorinating resp. sulphating roasting a post-oxidation ion, whereby magnetite is to a large extent converted to hematite. The Spanish patent document does not contain any further information regarding the degree of oxidation, i.e. it is not possible to deduce from the patent document how far the magnetite is to be converted to hematite. Namely, if magnetite is completely converted to hematite, then the post-oxidised burn contains practically no more sulphide sulphur, so that a chlorinating and sulphating roasting is no longer possible.
Det ble nu overraskende nok funnet at man kan unngå den-ne ulempe når man ved den i og for seg kjente etteroksydasjon sen-ker magnetittinnhold til 5 til 10 %, hvorunder sulfidsvovelrestinnholdet i den etteroksyderte avbrand synker til 1 til 2,5 %. It has now surprisingly been found that this disadvantage can be avoided when the magnetite content is lowered to 5 to 10% by post-oxidation known per se, during which the residual sulphide sulfur content in the post-oxidised burn-off drops to 1 to 2.5%.
Dette resultat var desto mere overraskende som det ikke var å vente at oksydasjonen av magnetitten forløper før en oksyda-sjon av det sulfidsvovel som fremdeles foreligger i avbranden. This result was all the more surprising as it was not expected that the oxidation of the magnetite would proceed before an oxidation of the sulphide sulfur which is still present in the burn.
Som eksempel for fremgangsmåten ifølge oppfinnelsen er på hosføyede figur oppført resultatene av oppslutningsundersøkel-ser av i stigende grad etteroksydert avbrand, dvs. avbrand med avtagende magnetittinnhold. I det på figuren viste diagram er prosentinnholdet av kobber og sink i purpurmalm etter utlutning av røstegodset (ordinaten) vist i avhengighet av prosentinnholdet av Fe304 i avbranden før oppslutningsrøstningen (abscissen). As an example of the method according to the invention, the attached figure shows the results of digestion investigations of increasingly post-oxidised slag, i.e. slag with decreasing magnetite content. In the diagram shown in the figure, the percentage content of copper and zinc in purple ore after leaching of the roasting material (the ordinate) is shown as a function of the percentage content of Fe304 in the waste before the leaching roasting (the abscissa).
Av energiøkonomiske årsaker er det hensiktsmessig at den varme avbrand fra røstningen umiddelbart tilføres etter-oksy-dasjonstrinnet. For energy-economic reasons, it is appropriate that the hot waste from the roasting is immediately supplied to the post-oxidation step.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19681805077 DE1805077B1 (en) | 1968-10-25 | 1968-10-25 | Process to improve the digestion of chlorinated, roasted non-ferrous metal-containing gravel waste with high magnetite content |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| NO123726B true NO123726B (en) | 1972-01-03 |
Family
ID=5711457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO401769A NO123726B (en) | 1968-10-25 | 1969-10-08 |
Country Status (9)
| Country | Link |
|---|---|
| BE (1) | BE740744A (en) |
| DE (1) | DE1805077B1 (en) |
| ES (1) | ES362058A1 (en) |
| FR (1) | FR2021547A1 (en) |
| GB (1) | GB1280546A (en) |
| NL (1) | NL6916098A (en) |
| NO (1) | NO123726B (en) |
| RO (1) | RO55432A (en) |
| SE (1) | SE352901B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5722710Y2 (en) * | 1978-10-05 | 1982-05-17 | ||
| DE3318137C2 (en) | 1983-05-18 | 1986-07-31 | Erni Elektroapparate Gmbh, 7321 Adelberg | Multipole electrical connector |
-
1968
- 1968-10-25 DE DE19681805077 patent/DE1805077B1/en active Pending
-
1969
- 1969-01-02 ES ES362058A patent/ES362058A1/en not_active Expired
- 1969-10-08 NO NO401769A patent/NO123726B/no unknown
- 1969-10-16 RO RO6128469A patent/RO55432A/ro unknown
- 1969-10-20 SE SE1436869A patent/SE352901B/xx unknown
- 1969-10-22 FR FR6936183A patent/FR2021547A1/fr not_active Withdrawn
- 1969-10-24 NL NL6916098A patent/NL6916098A/xx unknown
- 1969-10-24 BE BE740744D patent/BE740744A/xx unknown
- 1969-10-24 GB GB5213469A patent/GB1280546A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| NL6916098A (en) | 1970-04-28 |
| GB1280546A (en) | 1972-07-05 |
| SE352901B (en) | 1973-01-15 |
| ES362058A1 (en) | 1970-11-01 |
| FR2021547A1 (en) | 1970-07-24 |
| BE740744A (en) | 1970-04-24 |
| DE1805077B1 (en) | 1970-06-04 |
| RO55432A (en) | 1973-08-20 |
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